Enzymatic detection of As(III) in aqueous solution using alginate immobilized pumpkin urease: Optimization of process variables by response surface methodology

Urease immobilized on alginate was utilized to detect and quantify As³⁺ in aqueous solution. Urease from the seeds of pumpkin (vegetable waste) was purified to apparent homogeneity by heat treatment and gel filtration (Sephadex G-200). Further enzyme was entrapped in 3.5% alginate beads. Urea hydrolysis by enzyme revealed a clear dependence on the concentration and interaction time of As³⁺. The process variables effecting the quantitation of As³⁺ was investigated using central composite design with Minitab^® 15 software. The predicted results were found in good agreement (R² = 96.71%) with experimental results indicating the applicability of proposed model. The multiple regression analysis and ANOVA showed that enzyme activity decreased with increase of As³⁺ concentration and interaction time. 3D plot and contour plot between As³⁺ concentration and interaction time was helpful to predict residual activity of enzyme for a particular As³⁺ at a particular time.     

Response surface design for the optimization of enzymatic detection of mercury in aqueous solution using immobilized urease from vegetable waste

Soluble and alginate immobilized urease was utilized for detection and quantitation of mercury in aqueous samples. Urease from the seeds of pumpkin, being a vegetable waste, was extracted and purified to apparent homogeneity (sp. activity 353 U/mg protein; A₂₈₀/A₂₆₀ = 1.12) by heat treatment at 48 ± 0.1 °C and gel filtration through Sephadex G-200. Homogeneous enzyme preparation was immobilized in 3.5% alginate leading to 86% immobilization, no leaching of enzyme was found over a period of 15 days at 4 °C. Urease catalyzed urea hydrolysis by soluble and immobilized enzyme revealed a clear dependence on the concentration of Hg²⁺. Inhibition caused by Hg²⁺ was non-competitive (K_i = 1.2 × 10⁻¹ μM for soluble and 1.46 × 10⁻¹ μM for alginate immobilized urease.). Time-dependent inhibition both in presence and in absence of Hg²⁺ ion revealed a biphasic inhibition in activity. For optimization of this process response surface methodology (RSM) was utilized where two-level-two-full factorial (2²) central composite design (CCD) has been employed. The regression equation and analysis of variance (ANOVA) were obtained using MINITAB^® 15 software. Predicted values thus obtained were closed to experimental value indicating suitability of the model. 3D response surface plot, iso-response contour plot and process optimization curve were helpful to predict the results by performing only limited set of experiments.     

Detection of copper (II) in aqueous solution by immobilized urease obtained from agro-waste: Optimization of process variables

Urease was used for estimation of Cu²⁺ in aqueous solution. Process variables were optimized by Central Composite Design using MINITAB® 15 software. Results predicted by the design were close to experimental value indicating suitability of the model. 3D surface plot and isoresponse contour plot were helpful in predicting results by performing limited set of experiments. Urease was extracted from discarded seeds of pumpkin to apparent homogeneity by heat fractionation and gel filtration. Homogeneous enzyme preparation was further immobilized in 3.5% alginate. Effect of Cu²⁺ on the activity of soluble and immobilized enzyme was investigated. Enzyme inhibition was biphasic, irreversible, and non-competitive (Ki = 1.06 μM).     

Enzymatic detection of mercuric ions in ground-water from vegetable wastes by immobilizing pumpkin (Cucumis melo) urease in calcium alginate beads

Present report describes a quick and simple test based on enzyme inhibition for the detection of mercury in aqueous medium by urease immobilized in alginate beads. Urease was extracted from the discarded seeds of pumpkin (Cucumis melo) and was purified to apparent homogeneity (5.2-fold) by heat treatment at 48+/-0.1 degrees C and gel filtration through Sephadex G-200. The homogeneous enzyme preparation (Sp activity 353 U/mg protein, A(280)/A(260)=1.12) was immobilized in 3.5% alginate leading to 86% immobilization. Effect of mercuric ion on the activity of soluble as well as immobilized enzyme was investigated. Hg(2+) exhibited a concentration-dependent inhibition both in the presence and absence of the substrate. The alginate immobilized enzyme showed less inhibition. There was no leaching of the enzyme over a period of 15 days at 4 degrees C. The inhibition was non-competitive and the K(i) was found to be 1.26x10(-1)microM. Time-dependent interaction of urease with Hg(2+) exhibited a biphasic inhibition behavior in which approximately half of the initial activity was lost rapidly (within 10 min) and reminder in a slow phase. Binding of Hg(2+) with the enzyme was largely irreversible, as the activity could not be restored by dialysis. The significance of the observations is discussed.     

Enzymatic detection of heavy metal ions in aqueous solution from vegetable wastes by immobilizing pumpkin (<Emphasis Type="Italic">Cucumis melo</Emphasis>) urease in calcium alginate beads

Enzyme urease is extracted from the discarded seeds of pumpkin. Urease was purified to apparent homogeneity (5.2 fold) by heat treatment at 48 ± 1°C and gel filtration through Sephadex G-200. Effect of model metal ions on the activity of the homogeneous enzyme preparation (sp. activity 353 U/mg protein, A₂₈₀/A₂₆₀ = 1.12) of soluble as well as immobilized enzyme was investigated. The soluble and immobilized urease has been used for the quantitative estimation of general water pollution with heavy metal ions like Hg²⁺, Cu²⁺, Cd²⁺, and Co²⁺. The measurements of the urease residual activity have been carried out in tris-acetate buffer after pre-incubation of model metal salt. The inhibition was found to be biphasic with an initial rapid loss of activity and remainder in slow phase of 10∼15 min. The immobilization was done in 3.5% alginate beads leading to 86% of entrapment. There was no leaching of the enzyme over a period of 15 days at 4°C. The beads were fairly stable up to 50°C and exhibited activity even at −10°C. The inhibition by these ions was non-competitive and irreversible, hence could not be restored by dialysis. Based on the values of inhibition constant Ki the heavy-metal ions were found to inhibit urease in the following order Hg²⁺ > Cu²⁺ > Cd²⁺ > Co²⁺.     

Purification of a moderate thermotolerant Bacillus coagulans BTS1 lipase and its properties in a hydro-gel system

An alkaline thermotolerant lipase of Bacillus coagulans BTS1 was successively purified by ammonium sulfate precipitation and DEAE anion exchange chromatography. The purified lipase immobilized in alginate beads showed an optimal activity at pH 7.5 and 55 degrees C. A pH of 5.0 or 10.0 completely quenched the activity of immobilized lipase. The alginate-bound lipase retained its activity following exposure to most of the organic solvents including amines, alkanes and alcohols. Chloride salt of Al3+, Co2+, Mg2+ and NH4+ modulated the lipase activity of alginate-immobilized enzyme. The alginate entrapped lipase showed a preferentially high activity towards p-nitrophenyl palmitate (C: 16) and activity of matrix increased following exposure to SDS. Moreover, the immobilized lipase retained more than 50% of its activity after 3rd cycle of reuse.     

Various properties of immobilized AMP-aminohydrolase

Properties of immobilized AMP-aminohydrolase from rabbit muscles are studied. The enzyme retains its activity for a year, is stable under manifold treatment with the substrate or under single treatment with 1 M NaCl which contains 50% ethylene glycol or 10% isopropanol and under treatment with 5 M K2 HPO4 (pH 8.5). The established pH-optimum (6.5-7.0) and the temperature optimum (30-40 degrees C) for immobilized AMP-aminohydrolase as well as inhibition of its activity by Co2+, Cd2+, Zn2+ and n-chloromercury benzoate indicate similarity of its properties with those of the purified enzyme.     

Characterization of dextransucrase immobilized on calcium alginate beads from Leuconostoc mesenteroides PCSIR-4

Immobilization of dextransucrase from Leuconostoc mesenteroides PCSIR-4 on alginate is optimized for application in the production of dextran from sucrose. Dextransucrase was partially purified by ethanol upto 2.5 fold. Properties of dextransucrase were less affected by immobilization on alginate beads from soluble enzyme. Highest activities of both soluble and immobilized dextransucrase found to be at 35 degrees C and optimum pH for activity remain 5.00. Substrate maxima for immobilized enzyme changed from 125 mg/ml to 200 mg/ml. Incubation time for enzyme-substrate reaction for maximum enzyme activity was increased from 15 minutes to 60 minutes in case of immobilized enzyme. Maximum stability of immobilized dextransucrase was achieved at 25 degrees C with respect to time.     

Utilization of an exopolysaccharide produced by Chryseomonas luteola TEM05 in alginate beads for adsorption of cadmium and cobalt ions

Cadmium and cobalt adsorption from aqueous solution onto calcium alginate, sodium alginate with an extracellular polysaccharide (EPS) produced by the activated sludge bacterium Chryseomonas luteola TEM05 and immobilized C. luteola TEM05 was studied. In addition, solutions containing both of these ions were prepared and partial competitive adsorption of these mixtures was investigated. Metal adsorption onto gel beads was carried out at pH 6.0 and 25 degrees C. The maximum adsorption capacities determined by fitting Langmuir isotherms to the data for calcium alginate, calcium alginate+EPS, calcium alginate + C. luteola TEM05 and calcium alginate + EPS + C. luteola TEM05 were 45.87, 55.25, 49.26, 51.81 mg g(-1) for Co(II) and 52.91, 64.10, 62.5, 61.73 mg g(-1) for Cd(II), respectively. The biosorption capacity of the carrier for both metal ions together in competition was lower than those obtained when each was present alone.     

Production of lipase in a fermentor using a mutant strain of Corynebacterium species: its partial purification and immobilization

Extracellular Corynebacterium lipase was produced using a 2.5 L Chemap fermentor using 1300 ml fermentation medium at temperature 33 degrees C, agitator speed 50 rpm, aeration rate 1 VVM having KLa 16.21 hr(-1). Crude lipase was purified by salting out method followed by dialysis and immobilized using calcium alginate gel matrix followed by glutaraldehyde cross linking Purification process increased specific activity of enzyme from 2.76 to 114.7 IU/mg. Activity of immobilized enzyme was 107.31 IU/mg. Optimum temperature for purified and immobilized enzyme activity were 65 degrees and 50 degrees C respectively. Optimum pH was 8.0 in both the cases, Km and Vmax value for purified lipase were 111.1 micromol/min and 14.7% respectively. Ca2+ (5 mM) was found to be stimulator for enzyme activity. Immobilized lipase retained 68.18% of the original activity when stored for 40 days.     

Immobilization of carbonic anhydrase in alginate and its influence on transformation of CO2 to calcite

Present investigation entails carbonic anhydrase (CA) immobilization and its influence on transformation of CO₂ to calcite. CA enzyme was immobilized in alginate beads, subsequently maintained its catalytic efficiency after sequential operational cycles. The immobilized beads showed better operational stability by retaining nearly 67% of its initial activity even after six cycles. Batch scale studies with free and immobilized enzyme revealed that the entrapped CA hydrates CO₂ to bicarbonate and/or carbonate which was then made to react with Ca²⁺ ions to transform into calcite. Calcite was characterized by X-ray diffraction (XRD) and scanning electron microscopy (SEM). The entrapped CA was employed for the performance evaluation with respect to several operational parameters including the influence of enzyme concentration in free and immobilized condition. It was concluded that immobilized CA in alginate beads would have the potential for CO₂ sequestration by biomimetic route.     

Comparison of some properties of free and immobilized alpha-amylase by Aspergillus sclerotiorum in calcium alginate gel beads

Some properties of immobilized alpha-amylase by Aspergillus sclerotiorum within calcium alginate gel beads were investigated and compared with soluble enzyme. Optimum pH and temperature were found to be 5.0 and 40 degrees C, respectively, for both soluble and immobilized enzymes. The immobilized enzyme had a better Km value, but kcat/Km values were the same for both enzymes. Entrapment within calcium alginate gel beads improved, remarkably, the thermal and storage stability of alpha-amylase. The half life values of immobilized enzyme and soluble enzyme at 60 degrees C were 164.2, and 26.2 min, respectively. The midpoint of thermal inactivation (Tm) shifted from 56 degrees C (for soluble enzyme) to 65.4 degrees C for immobilized enzyme. The percentages of soluble starch hydrolysis for soluble and immobilized alpha-amylase were determined to be 97.5 and 92.2% for 60 min, respectively.     

Purification and properties of alpha-galactosidase from white-rot fungus Pleurotus florida

alpha-Galactosidase was strongly induced in the white-rot fungus Pleurotus florida by arabinose than its natural substrates and was purified to homogeneity by acetone precipitation, ultrafiltration and DEAE-Sepharose chromatography. The enzyme was a monomeric protein with a molecular mass of approximately equal to 99 kDa, as revealed by native-PAGE and SDS-PAGE. alpha-Galactosidase was optimally active at 55 degrees C for the hydrolysis of p-nitrophenyl-alpha-galactopyranoside (PNPalphaG) and lost its 20% and 50% of original activity in 30 min at 60 degres C and 70 degrees C, respectively. The pH optimum of the enzyme was between 4.6 and 5.0. It was stable in a wide pH range (pH 4.0 to 9.0) at 55 degrees C for 2 h. The Ag+ and Hg2+ strongly inhibited the enzyme activity. Galactose, glucose, maltose and lactose also inhibited the enzyme activity, whereas N-bromosuccinimide treatment resulted in near total loss of acitivity. The Km and Vmax values of the enzyme for PNPalphaG were found to be 1.1 mM, and 77 micromol min(-1) mg(-1), respectively. alpha-Galactosidase immobilized in agar was more effective for the degradation of raffinose than in the sodium alginate. TLC results indicated its potential for the removal of raffinose and stachyose in soymilk.     

Preparation and properties of an immobilized pectinlyase for the treatment of fruit juices

Pectinlyase, present in different commercial pectinases used in juice technology, was immobilized on alginate beads. The optimal conditions were: 0.17 g alginate ml(-1), 1.2% (w/v or v/v) enzyme concentration and acetic-HCl/glycine-HCl buffer at pH 3.6 or tris-HCl/imidazole buffer at pH 6.4. Maximum percentage of immobilization (10.6%) was obtained with Rapidase C80. Kinetic parameters of free and immobilized pectinlyase were also determined. The pH and temperature at which activity of soluble and immobilized enzyme was maximum were 7.2 and 55 degrees C. Thermal stability was not significantly altered by immobilization, especially at 40 degrees C, showing two periods of different stability. Free and immobilized preparation reduced the viscosity of highly esterified pectin from 1.09 to 0.70 and 0.72 mm(2) s(-1), respectively, after 30 min at 40 degrees C. Furthermore, the immobilized enzyme could be re-used through 4 cycles and the efficiency loss in viscosity reduction was found to be only 9.2%.     

A simple laboratory experiment for teaching enzyme immobilization with urease and its application in blood urea estimation

An experiment is described in which students carry out urease purification, immobilization and its application in blood urea estimation. Urease from pigeonpea is partially purified using acetone fractionation and then immobilized on calcium alginate in the form of beads. The immobilized enzyme has a better shelf-life at 4°C than soluble enzyme. Various aspects of enzyme immobilization are discussed. Blood urea estimation is carried out with immobilized enzyme beads and the beads can be used repeatedly for this purpose making it an economical procedure compared to commercial kits.     

Acetohydroxamate inhibition of the activity of urease from dehusked seeds of water melon (Citrullus vulgaris)

Urease from the seeds of watermelon (Citrullus vulgaris) was purified to apparent homogeneity, using two acetone fractionation steps, heat treatment at 48 degrees C and gel filtration through Sephadex G-200. Effect of acetohydroxamic acid (AHA) on the activity of the homogeneous enzyme preparation (sp. act. 3000 +/- 550U/mg protein) was investigated. AHA exhibited a concentration-dependent inhibition both in the presence and absence of the substrate. The inhibition was uncompetitive and the Ki was 2.5 mM. Binding of AHA with the enzyme was reversible, as 63% activity could be restored by dialysis. Time-dependent inhibition revealed a monophasic inhibition of the activity. Addition of beta-mercaptoethanol (ME) gradually abolished the inhibition. Pre-treatment of native enzyme with 8.0 mM ME for 5 min at 30 degrees C exhibited protection against AHA-induced inhibition. The significance of these observations is discussed.     

锰过氧化物酶的耦合固定化及其性质研究

分别采用海藻酸钠、明胶和壳聚糖为载体,并以戊二醛为交联剂,通过包埋-交联和吸附-交联两种耦合固定化方法制备固定化锰过氧化物酶。探讨了酶的不同固定化条件和固定化酶的部分性能。与游离酶相比,制备的3种固定化酶最适反应pH分别由7·0降低到5·0、5·0和3·0,最适反应温度分别由35℃升高到75℃、55℃和75℃。3种固定化酶的耐热性都显著提高,其中用壳聚糖制成的固定化酶在pH2·2~11的宽范围内表现出很好的酸碱耐受性。30℃连续测定6~9次酶活力,重复使用的3种固定化酶显示出良好的稳定性。将固定化酶应用在偶氮染料的脱色中,用明胶制成的固定化酶在静置和摇床条件下,以及用海藻酸钠制成的固定化酶在摇床条件下,均表现出与游离酶相近的脱色能力,并且在重复进行的摇床实验中,脱色能力未降低,反应前后的酶活力均没有损失。     

Substituted polymethylglutamate membrane for immobilization of urease

Poly-γ-methyl-l-glutamate (PMG) was modified and used for enzyme immobilization. Trichloroethyl ester (TCE) and three kinds of amino groups (ethylenediamine, ED; 1,8-diamino-4-amino-methyloctane, TA; polyethyleneimine, PEI) were introduced into the pendant group of PMG. A membrane was prepared from these polymers for enzyme immobilization. Urease was immobilized on each membrane using glutaraldehyde or water-soluble carbodiimide. Urease was very stable when it was immobilized with water-soluble carbodiimide on the membrane having PEI in the pendant group. The characteristics of immobilized urease were also discussed.     

Short Communication: Immobilization of urease from pigeonpea (Cajanus cajan L.) on flannel cloth using polyethyleneimine

Urease of pigeonpea has been immobilized on polyethyleneimine-activated cotton cloth followed by cross-linking with dimethyl suberimidate. Optimum immobilization (56%) was obtained at a protein loading of 1.2mg/5×5cm2 cloth piece. The immobilized enzyme stored in 0.1M Tris/acetate buffer, pH6.5, at 4°C had a t1/2 of 70 days. There was practically no leaching of the enzyme from the immobilization matrix in 15 days. The immobilized enzyme was used 7 times at an interval of 24h between each use with 75% residual activity at the end of the period. Blood urea analysis was carried out with immobilized urease for some clinical samples.     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.